Buttermaking means



H. c. HORNEMAN ETAL 2,395,051

BUTTER MAKING MEANS Filed Dec. 1s, 1941 2 sheets-sheet 1 Feb. 19,v 1946.

Feb. 19, 1946.

H. c HORNEMAN ETAL 2,395,051

BUTTER MAKING MEANS 2 Sheets-Sheet 2 I Filed DSG. 15, 1941 Pnenad i=eb. 19,194s;

slgnmen alto''hei'ryf '.iirell CorporatiomChL cago, 111 arcor-poration@Delaware lamil and'ernard W. y

lbutter-making processes, and' itrhas-partlcular'-` 1 relation to` a method of, and apparatus fonde-5 i veloping a .true lbutter texture in -buttermade according to such continuous procesess'.V I,'`;'

`Substantial progress has been made inr recentv years in developing continuous butter-making? processes. The primary object ofv this devellzip--f ment has been to-overcome thedimcultie's .and f objections associatedwiththe prior art method of making butter which involved"y the churninglof -f large batches of cream into-butter. Except f or the increased scale on which the operationwas carried out, this-prior4 art methodv of .making'"' butter on acorn'mercial scale bychurning reiv mained essentially theA same' as that used by small f dairymenand housewives from time immernorial.'

Shortly 'after theproduc'tion of --jbutter cna commercial scaledeveloped, it became apparent that it would be'agre'at advantage to be 'able to.'

produce butter .by a continuous process' as distingllished from 4theprior art churning loperav tion, which is classified es being an intermittent or batch type process. It is a'recognize'd principley of production engineering thatyherea prductis to be produced in largequantities'onfandom-1 j f.

Y mercial basis, axcontinuous, process hasfcertain, fj

inherent advantages overan intermittentor batch type procesa The principal advantagesjare that the continuous process gives a muchgreaterpro 1 vduction rate for the amount o f t equipr'i r 'ent ini- 1 i l l1-Ohms? (Cl-995244)?" v v n y `Our` invention relates generally 'to continuous so accustomed to butter having the texture of the e product'made byv churning that-buttermadeacf cording' to any otherprocss alsohadfto have this I same texture in order lto be salableand to meetv with llargejscale acceptance by the consumers.

Aecorqingm the' .object of our inventiem generallyvstated, is; the provision oan apparatus and method for developing a'true vand natural butter -'txt1. r e in continuous butter-making. processes. fthe iniientionfis not limi ted` to 'any particular type"v cfcontinuous butter-making: process, it 'has been butter i products made according to found to be' -parti,cul arly adapted; for' developing al *in-part,

volved, andwhat is .of equator-"greater importy ance, standardization and controlerthe v'product may bem'oreeasily and accurately carried-.out inf' '5 A i asjt'exture c eiopingjapparatus andjmethod acontinuous process. a-continuous process of maa.king"b'utterl has the possibltyofpermitting countered jinldevelopiiig a continuous butter-f making vprocessgwas thatofv obtaining la nal- .butter product which had a texture ,'corresr'ion'd ing to that of butter made bychurnin g. Although `several continuous processeswere suggested :and developed'wherein products could be" produced i which had a chemical compositioncorresponding to that'of ord-inarybutter asmade according "to the prior artchurningj processes, the physical` asr'aect of Such products were fundamentally cicerent fromcrqmarybutter-- insofar as we are s aware 'it was not possbleheretofore to produce a butter product. wltha continuous process that f '-40' i Fig. 3 .is an-fenl'argedfragmentary,,verticals `tional view -takenlthroughone qf; theeonneeuone between-the-different sections'off'theteidiure .fvelopero flig. 1 and showing the details:qf ne" of fthe texture .i developing '-"oriflces`- provided; r, v

AAVdisk infcontinuous process of toperati'on.; jinvolvin Y th onmn view`bfnieforficeeprdvidihg Although -Fig"; .51 is. aviewvsimiiar tong. axofamodineplf,

" form'offreezerunitadapted `to'intersperse a non;` 1

0 toxic; 'smoothnesslimparting gas into 'iagbutterj i -fccimxiositi'oiras'A Ait is chilledandsolidiied thereinl y In' makngbutterQ'by a continuous process, itis' f ,v-flrstj necessary to'fobtain.'v concentrated ,milk fat :in thefcontnuous phase. In cream, whichisthe `raw material in but'ter-making processes, the 'milk .phase. Although there are several possible-proc- .esses by which the phases in cream may be re-f versed so as to obtain the milk fat in concentrated form in the' continuous phase, the lprocess described in our above-mentioned .prior lapplication for -United States Letters Patent, Serial No. 368,750, provides a -very satisfactory method of.

obtainingthis product. In-l Fig. 1 ofthe drawings, the process of obtaining -milk ytattili the continuous phase disclosed in ourgabovefmentioned J application is combined with ,the texture developing feature of the present invention ,so as to'I obtain `a high quality butter product. 1t will, however, be understood that the texture developing feature of the present-invention is not limited solely to use in connectionwith the milk fat concentrating process described in.our'abovemen.

tioned application. i

Referring to Fig. 1 of the drawings, cream ordinarily of around 30-40 per cent milk fat' is warmed to about 90 to 110 F. Ain a pre-warming vat I0. (If neutralization of the cream is desired, it may be carried out, for example, in the pre-warming vat I in accordance with the general practices in the art.) From-the vat I0, the pre-warmedcream is pumped by a pump Il through a pipe line l2 into a lter I3. Steam at around 90-100 pounds per square inch pressure isintroduced into the line I2 from a steam supply line connected there with, as shown. The steam serves towarm the cream so that it enters the iilter I3 at around 135 F. The filtered cream is conducted from the iilter` I3` through a pipe line I5 into a hash pasteurizer unit I6 which may be of the well-known Jensen type. Steam is introduced into the line I5 from a steam supply line I1 and mixes with the ltered cream so that as it enters the bottom of the pasteurizer I6 it will be at a temperature of around 150 to 160 F. They cream ordinarily' remains in the pasteurizer I6 for about'ten to fifteen seconds'wherein it is heated to about 190 to 194 F., for example, by indirect steam. From the topofj the pasteurizer unit I6, the cream passes through a pipe line I8 'into a supply tank 20 Wherefrom it is ready to be delivered to a zoneof subatmospheric pressure or vacuum-steam treatment.

The pasteurized cream, ordinarily at around 175 to 190 F., is withdrawn from the supply tank through a pipe line 22 into a vacuum pasteurizer 23fwbich may be of the type described in detail in United States Patent 2,022,420, issued November 26, 1935, to Hammer, Horneman, and

Parker. The pressure in the pasteurizer or vacumn'chamber 23 is sub-atmospheric and is ordinarilymaintained at a vacuum of `around 25 to 26 inches of'mercury so that the temperature in the chamber will be around 130 F. lSteam at around 90 pounds per square inch pressure is introduced into the bottom of the pasteurizer 23 through a number of steam pipes 24, connected as shown,

whereby it comes into direct contact with the cream while at the reduced pressure. The desired -no loss or gain in its moisture content, co1- lects in the bottom of the chamber 23 and is pumped therefrom by a pump 26 through a pipe line l21 into a centrifuging separator 30; The tem- 4from the separator at 3l.

aeoaosi perature of the cream in the separator 30 is ordinarily around 125 F.. and in every case should v'be at least above the particular melting point of the milk fats present in the cream.

In the separator 30 (which may be of the ordinary centrifuge type) the milk fats are obtained in the continuous phase and are-separated from the protein, skim milk, etc. which are expelled The fat product containing about 80-98 pe;` cent milk fat, depending upon the extent of the centrifuging action, is withdrawn from the top of the separator 30 through a pipe line 32 into a milk fat storage tank 33. From the vat 33, the milk fats in the continuous phase and still in the liquid state are pumped by a pump 34 through interconnected pipes 35 and 36 into a mixing chamber or unit 31. A vat serves to hold a controlled aqueous solution of salt and starter flavor, etc., which may be pumped at a predetermined rate by a. pump 4I through a pipe line 42 and the line 36 into the mixing chamber 31 wherein it is thoroughly mixed with the incoming fat from the vat 33. The resulting butter-forming mixture leaving the mixing chamber 31, and ordinarily containing at least 80 per cent milk fat,`is delivered through a. pipe line 43 by a pump 44 into a freezer unit 45. In the freezer unit 45, the liquid butter-forming mixture is solidied or chilled so as to form a. brittle, waxy, oily tasting mass. The pressure from the pump 44 serves to force this brittle, waxy mass through our texture developer unit indicated generally at 46, wherein a true butter texture is developed therein. The butter leaving the texture developer unit 46 is delivered to a, packaging machine 41. freezer unit 45 and our texture developer unit 46 are described in detail hereinafter.

It will be understood that the above detailed process of obtaining concentrated milk fat in a continuous manner is intended to be illustrative and that certain other methods of obtaining con'- centrated milkr fat in a continuous phase from cream may be used.` Likewise, the temperatures and pressures above cited in connection with the operation of the vacuum pasteurizer 23 and the centrifugal separator 30, are illustrative of typical operating conditions, and certain other values of temperature and pressure may be used depending upon conditions involved. e

The change in the cream during the vacuumi steam treatment above described is not fully understood. Our investigations indicate that subjecting the creamto the sub-atmospheric pressure produces an expansion of the cream and that the action of the steam (e. g. high pressure steam of around 90 to 100 pounds per square inch back of the valve) coming into direct contact with the cream while in the expanded stage modifies the milk fat globules so that they separate in the continuous phase when subjected to the centrifuging action inthe separator 30. Our investigations also indicate that the best results are obtained when the cream entering the zone of sub-atmospheric pressure is pre-heated to aV temperature greater than the temperature of saturated steam at the reduced pressure. The fact that the fat is obtained in the continuous phase indicates that the complex protein-fat hull or membrane surrounding the milk fat globules is modiiied physically, or chemically, or both,'

The details of construction of the -to the concentrated fat in the mixing unit 51 makes possible a more uniform and finer dispersion of water in fat, resulting finally in an improved butter texture. The amount oi water or aqueous solution added varies with the percentage of milk fat in the concentrate from the vat 5I (ordinarily around 85-95 per cent) and is controlled so that the final product ordinarily contains at least 80 per cent milk fat.

Furthermore, our particular process produces a more stable butter due both to the fine dispersion of the water through the continuous fat phase, and to the low protein content oi' the milk fat. In this latter connection, it will be noted that a substantial proportion of the nitrogenous or protein material-one of the bacteria foods of butter-is separated from the milk fat in the centrifuging separator 55. The process also produces a more uniform butter due to the removal of the original water and the water soluble materials in the'cream, which, as obtained '25 in practice, contains only around per cent of the desired milk fat. The advantage is obtainable by separating out the original non-fat materials and replacing them with controlled aqueous starter mixtures free from undesired contamination, as will be obvious to those skilled in the art. An additional advantage resides in the elimination of churning" carried out today for the most part in bacteria contaminated wooden churns.

In the specification and claims, the term starter refers to starter cultures. These cultures are well known in the art and serve as ilavoring constituents or means in the manufacture of butter. Likewise, in the specification and claims the term cream refers to ordinary cream in which the milk fat is in the disperse phase, i. e., dispersed as an emulsion in a continuous phase of non-fat milk liquids.

Referring to Fig. 2 of the drawings, it will be seen that the freezer unit comprises an inner cylinder 55 in which the butter-forming mixture pumped from the mixing tank 31, Fig. l, is chilled and solidied. A brine jacket 5| is disposed around the inner cylinder so that a refrigerant may be circulated in heat conductive relationship with the inner cylinder 58. The brine chamber 5I is covered with insulation or lagging 52, and refrigerant inlet and outlet openings and 54, respectively, are provided adiacent the opposite ends of the jacket 5| for delivery to and withdrawal of refrigerant from the freezer 45. Brine serves very satisfactorily as a refrigerant for use in the freezer unit 45.

The inner freezing cylinder 50 is closed at its opposite ends by a pair of heads 55 and 55 connected in flange to flange relationship therewith, as shown. The head 55 attached to the lefthand end of the cylinder 55 has an inlet opening or connection 51 integrally formed as part thereof and to which the butter-forming mixture pipe line 45 is connected. The right-hand head 55 is provided with a jacketed outlet connection 55 through which the chilled and solidifled mass may be delivered to the texture developer unit 48. Central openings are provided through each of the head units 55 and 58 so as to accommodate a hollow shaft 50 which passes longitudinally through the freezer unit 45. The shaft 55 is journalled in the heads 55 and 58, which serve as bearings therefor. A pair of stuillng boxes 5i and 52 are provided on each end of the heads 55 and 58, respectively, so as to provide a iluid tight seal about the rotating shaft 80.

A helical screw 85 is carried on the shaft 80 within the freezing chamber 50` as shown. The function of the screw 85 is to scrape the chilled butter-forming mixture from the inner surface of the chamber 58 where it is solidified, and also to aid in forcibly feeding the material from left to right through the freezer unit 45. The screw 55 also acts as an agitator for the partially solidified and partially liquid butter-forming mass in the cylinder 50, particularly in the left-hand half thereof wherein a substantial portion of the contents are still in the liquid state. A pulley 88 is keyed to the left-hand end of the shaft outside of the freezer 45 so as to provide means for rotatably driving the shaft 60 and the screw 55 carried thereon.

The shaft 50 is preferably tubular or hollow so that hot water may be circulated th'erethrough for the purpose of melting oiI solidified butterforming mass which may be frozen on the shaft 58 or on the helical screw 55. This is particularly important in connection with the cleaning of the freezer unit 45 for it permits substantially all of th'e mixture in the cylinder 50 to be forced out the right-hand side thereof through the outlet connections 55.

As stated,vthe jacketed outlet connection 58 of the freezer unit 45 is connected with our novel texture developer unit 48, as shown in Fig. l of the drawings. The particular texture developer unit 45 shown is made in four sections each of which comprises an inner tube or conduit through which the butter-forming mass is fed, and an outer jacket for circulating water. One of the connections between these four sections is sh'own in detail in Fig. 3 of the drawings. As there shownl the lower end 1I of the inner pipe 18 in the upper section is counter-bored so as to t over the upper end 12 of the inner pipe 10 in the next lower section. A disk member 14, shown in plan view in Fig. 4, is supported in between the interiltting pipe ends 1I and 12, as shown. The disk member has a restricted slot-shaped orifice 15 centrally formed therein through which the butter mass is forced as it is fed through th'e texture developer 45. The disk member 14 is so machined and designed that it is generally cup-shaped with a short portion formed on the bottom thereof which fits into the pipe end 12, while an annular shoulder abuts against the top face of the pipe end 12. The upper edge of the disk member 14 ts accurately in a shoulder formed in the counter-bored pipe end 1| as indicated at 18. The inside of the disk member 14 is preferably smoothly cupped and rounded so as to present a funnel-shaped butter receiving end so that th'ere will be no sharp corners in which butter may be collected and retained.

The upper pipe 15 is surrounded by a jacket section 58 having an inset skirt 8| integrally formed on the lower end thereof which fits accurately within the upper end of a lower jacket section 55 surrounding the lower inner pipe 10. 'I'he jacket sections 80 are provided with opposing integral flanges 83 and 84 which are separated by a. gasket member 85. A number of swing clamps 55 are carried on the lower jacket section 85 below the flange 84 which are adapted to swing up around the flanges 83 and 84, as `,hown. A set screw 51 with a wing nut head is provided in a threaded hole in each of the clamp members 86 so that it may be tightened down against the upper face of the flange 93, as shown. Any suitable number of the clamps 86, such as three, four or flve, may be provided, as required.

Certain other types of connections between the different sections of the texture developer unit 46 may be used, but the design shown in Fig. 3 represents one satisfactory design which permits the sections to be conveniently and readily taken apart for cleaning and permits the convenient reassembly thereof.

Warm water may be supplied into the upper I end of the texture developer unit 46 through the annular passageway formed in an inlet connection 90, and may be withdrawn from the lower section through an outlet pipe 9 I. The inlet connection 90 comprises an inner pipe 13 which communicates with the inner pipe l in the top section of the developer unit 46, and an outer jacket 82 which connects into the uppermost jacket section 80. The pipe I3 is provided with a valve I9 adjacent to the inner pipe 10, as shown. The water supplied through the annular space between the inner pipe I3 and outer pipe 82 should be at such a temperature and should be circulated at such a rate that the solidified butter mass will be slightly warmed and melted at the interior surfaces of the inner pipes 'I0 in the different sections of the texture developer 46. This permits the butter material to slip easily through the unit.

Disk members similar to the disk 'I4 are provided in each of the three connections at 92, 93 and 94 between the foursections of the texture developer unit 46, each having a restricted slotshaped orifice similar to the orifice 15. Ordinarily it will be desirable to make the connection 92, 93 and 94 the same so th'at the parts may be interchanged. A fourth disk member (not shown) is provided at 95 at the lower end of the texture developer unit where the bottom section connects with an outlet fitting 96.

The orifice in the disk member at the connection 95 may be circular instead of slot-shaped. and may be somewhat smaller than the other slot-shaped orices I5 in the other disk members 14 at the connections 92, 93 and 94.A For example, the slot-shaped orifices I5 in the disk members 'I4 (Fig. 4) may be 1" x 1%", while the orifice in the disk member in the connection 95 may be in diameter.

The pressure from the delivery pump 44, togeth'er with the action of the screw 65 in the freezer unit 45, serve to forcibly feed the solidified butter-forming mass through the texture developer 'unit 46. When this mass leaves the freezer 45, it is in the form of a brittle, waxy mass, which is oily to the taste. As this mass is forced through' the spaced-apart orifices provided in the texture developer unit 46, a true butter texture is developed therein. The exact reason and nature of the method in which the butter texture is developed in the mass as it passes through the orices is not fully understood. Apparently, the minute droplets or globules of water or aqueous mixture are interspersed uniformly through the milk fat portion of the mass in a size which corresponds to that of the water portion of churned butter. In any event, a high grade natural butter texture may be developed in what was a brittle, waxy mass as it passes through the unit 46.

In certain instances it may be desired to intersperse a non-toxic, smoothness-imparting gas into the liquid butter-forming mixture as it is 75 ceiving end being merged into the inside walls solidified or chilled. In Fig. 5 of the drawings, a freezer unitis indicated generally at |09 in which an inert gas such as nitrogen may be invided leading into the lower left-hand end of` the inner freezing chamber through which an inert gas such as nitrogen may be injected into the freezing chamber. The connection |0| connects with one side of a T-iitting |02 while a gas inlet pipe |03 having a valve |04 therein connects with the opposite side of the fitting |02. A pipe line |05 having a valve |06 therein is connected into the left-hand side of the tting |02 and serves from time to time as an inlet for supplying warm water or steam into the freezing chamber for the cleaning thereof.

A modified form of helical screw ||0 is provided onJ the tubular shaft running longitudinally to the freezer |00. The screw ||0 is made up of a number of short blades III each of which is carried on a hub member I|2 fastened on the longitudinal tubular shaft |09. The blades III are spaced a short distance apart, but in their general outline form a helical screw corresponding to the screw in Fig. 2. The spacing between the blades |I| increases the chopping or agitating action of the screw ||0 and serves to uniformly intersperse the inert gas entering the inlet connection I0| through the butter-forming mixture as it is solidified within the freezer unit |00.

Since certain further changes may be made in the foregoing construction and different embodiments of our invention may be made without departing from the scope thereof, it is intended that all matters described hereinbefore or shown in the accompanying drawings shall be interpreted as illustrative and not in a limited sense.

We claim:

1. Apparatus for converting a brittle, solidified butter mix into smooth textured, spreadable butter, comprising an elongated conduit, an elementv intermediate the ends of said conduit and having a single passageway of substantially less crosssectional area than the corresponding cross-sectional area of said conduit on opposite sides of said element, and means for feeding the butter mix through said conduit and passageway.

2. Apparatus for converting a brittle, solidified butter mix into smooth textured, spreadable butter, comprising an elongated conduit, an element intermediate the ends of said conduit and having a single passageway of substantially less crosssectional area than the corresponding cross-sectional area of said conduit on ODDOsite sides of said element, and means for feeding the butter mix through said conduit and passageway, said element having a funnel-shaped receiving end for guiding the butter mix to said passageway.

3. Apparatus for converting a brittle, solidified butter mix into smooth textured, spreadable butter, comprising an elongated conduit, an element intermediate the ends of said conduit and having a single passageway of substantially less. crosssectional area than the corresponding cross-sectional area of said conduit on opposite sides of said element, and means for feeding the butter mix through said conduit and passageway, said element having a funnel-shaped receiving end for guiding the butter mix to said passageway, the inside wall of said funnel-shaped reof said conduit and passageway so as to avoid the formation of any butter mix trapping pockets in said conduit.

4. Apparatus for converting a brittle, solidied butter mix into smooth textured, spreadable butter, comprising a conduit, an element in said conduit having a single passageway of substantially less cross-sectional area than the corresponding cross-sectional area of said conduit, and disposed substantially coaxially with said conduit, said element having a funnel-shaped receiving end for guiding the butter mix into said passageway, the inside wall of said funnel-shaped receiving end being merged into the inside walls of said conduit and passageway so as to avoid the formation of any butter mix trapping pockets in said conduit, and means for feeding the butter mix through said conduit and passageway.

5. Apparatus for converting a brittle, solidified butter mix into smooth textured, spreadable butter, comprising an elongated conduit, a plurality of elements respectively disposed in longitudinal- 1y spaced portions of said conduit, each of said elements having a passageway of substantially less cross-sectional area than the cross-sectional area of said conduit, and means for feeding the butter mix through said conduit and .through the passageways of said elements.

6. Apparatus for converting a brittle, solidified butter mix into smooth textured, spreadable butter, comprising an elongated conduit of cylindrical cross section, a plurality of elements respectively disposed in longitudinally spaced portions of said conduit, each of said elements having a passageway of substantially less cross-sectional area than the cross-sectional area of said conduit, the passageway in each of said 'elements being slot-shaped in cross section, and means for feeding the butter mix through said conduit and through the passageways of said elements.

7. Apparatus for converting a brittle, solidiiied butter mix into a smooth textured` spreadable butter, comprising a conduit of selected crosssectional area, means in said conduit for substantially reducing the eiiective internal cross-sectional area of a portion thereof intermediate its ends, and means for feeding the butter mix through said conduit at a predetermined rate sufficient to cause the butter mix to pass through the reduced portion of the conduit with a substantially accelerated velocity relative to the velocity of its movement in the normal portions of the conduit on opposite sides of said means.

8. Apparatus for converting `a brittle solidiiied butter mix into a smooth textured. spreadable butter, comprising an elongated conduit, means for feeding said butter mix through said conduit, and a plurality of elements respectively disposed in longitudinally spaced portions of said conduit, said elements extending transversely of the conduit and having passageways through which the butter mix is successively fed, the passageways in said elements being of substantially less cross sectional area than said conduit and one of said elements having a passageway of smaller cross sectional area than a preceding element.

9. Apparatus for texturating butter comprising, in combination, an elongated tubular element through which butter may be fed, pressure applying means for feeding butter to be texturated into and through said tubular element at a predetermined rate, and cup-shaped means for substantially reducing the eilective internal cross-sectional area of a portion of said tubular element intermediate the ends of said tubular element.

10. Apparatus for texturating butter comprising, in combination, an elongated tubular texturating element through which butter may be fed, pressure applying means for feeding butter to be texturated into and through said tubular element, and means for substantially reducing the effective internal cross-sectional area. of a portion of said tubular element intermediate the ends of said tubular element, said last mentioned means having a cup-shaped receiving end for guiding butter through the portion of said tubular element having the reduced internal crosssectional area.

11. A texturating device of the class described comprising, .in combination, a sectional elon- ,gated conduit, an element intermediate the ends of said conduit and having an opening therethrough of substantially less cross-sectional area than the unobstructed cross-sectional area of said conduit on opposite sides of said element, and means for feeding material to be texturated to and through said conduit and said element, said element being positioned in said sectional conduit at an end of a section thereof.

HERMAN C. HORNEMAN. RALPH V. HUSSONG. SIDNEY N. QUAM.

BERNARD W. HAMIVIER.

lCevrt-iicatc of Correction Patent No. 2,395,051. HERMAN C. HORNEMAN ET AL.

It is hereb certified that the above numbered patent was erroneously issued to Cherry-Burrel Corporation, of Chica o, Illinois, a corporation 0f Delaware, assignee by mesme assignments, Whereas sai patent should have issued to Sugar Creek Creamery Company, of Danville, Illinois, a corporation of Delaware, and Cherry-Burrell Corporation, of Chica/1o, Illinois, a corporation of Delaware, as 'oint owners, being assignees by direct and mesne assignments, as shown by the record of assignments in this olice; in the grant, line 15, for Cherry-Burrell Corporation, its successors read Sugar Creelt` Creamery Company, and Cherry-Burrell Corporation, as joint owners,'their successors; page 1, second column, line 19, immediately following the words is a continuation in part. insert the following paragraph February 19, 1946.

The aspects of this invention directed to the continuons process of maling batterare I disclosed and claimed in our Divisional Application Serial No. 626,234, jiled November 2, 1945.; and that the said `Letters Patent should be read with these corrections therein that the same may conform to the record of the case in the Patent Ofce.

Signed and sealed this 6th day of August, A. D. 1946.

LESLIE FRAZER,

First Assistant Commissioner of Patente. 

